US20170001359A1 - Polymeric multilayer films and methods to make the same - Google Patents
Polymeric multilayer films and methods to make the same Download PDFInfo
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- US20170001359A1 US20170001359A1 US15/038,880 US201415038880A US2017001359A1 US 20170001359 A1 US20170001359 A1 US 20170001359A1 US 201415038880 A US201415038880 A US 201415038880A US 2017001359 A1 US2017001359 A1 US 2017001359A1
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Links
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- B29K2995/00—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
- B29K2995/0001—Properties of moulding materials, reinforcements, fillers, preformed parts or moulds having particular acoustical properties
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Definitions
- Perforated films are typically used in the personal hygiene field providing a fluid transfer film allowing the fluid to be removed from areas near to the skin and into the absorbent area.
- Other common applications are in the food packaging industry and more recently acoustics absorption.
- Perforated films for these applications are usually less than 100 micrometers (0.004 inch) thick (more typically less than 50 micrometers (0.002 inch) thick) and are made, for example, of olefins, polypropylene, or polyethylene.
- Typical processing methods to produce perforated films include; vacuum drawing of film into a perforated panel or roll, use of pressurized fluid to form and puncture the film, needle punching with either cold or hot needles, or lasers to melt holes in the film. These processes, however, tend to have processing limitations such a hole size, hole density, and/or film thickness of film.
- Vacuum or pressurized fluid forming of perforated films tends to be limited to relatively thin films (i.e., films less than 100 micrometers thick) due to the forces available to deform and puncture the film. Also materials used in this type of forming process tend to be limited to olefin-based polymers.
- Another characteristic of this type of process is the creation of a protrusion in the film where the film is stretched until a perforation is created. This protrusion can be an advantage in the case of fluid control where the protrusion can act as a directional flow control feature. However, it can also be a disadvantage in applications where a low pressure drop is desired. The protrusion creates an elongated hole thereby increasing the surface area and increase fluid drag.
- Needle punching processes are also largely used for relatively thin films, but film thicknesses up to about 254 micrometers (0.010 inch) are sometimes seen. Limitations with this process tend to include perforation diameter holes per unit area, and protrusions in the film.
- Laser perforation processes can provide relatively small holes (i.e., less than 50 micrometers), can perforate a wide range of thicknesses, can create perforations that are planar with the film surfaces (i.e., without the protrusions associated, for example, with needle punching processes).
- Limitations of laser perforation processes include the types of materials that suitable for the process, and processing speeds and costs.
- Laser perforation processes tend to be best suited for processing films from polyethylene terephthalate (PET), polyethylenenaphthalate (PEN), polycarbonate (PC), or other higher glass transition temperature materials. Lasers are often not very effective, for example, in perforating olefin-based materials.
- the present disclosure describes a polymeric multilayer film having first and second generally opposed major surfaces, and comprising first, second, and third layers, an array of blind openings between the first and second major surfaces, and an average thickness, wherein the first, second, and third layers each have a first average thickness excluding any thickness said first, second, and third layers having in any of the blind openings, wherein the first and second layers extend into the first average thickness of the third layer, wherein each of the first, second, and third layers each have a second average thickness (including a thickness of zero) in the blind holes, wherein the second average thickness of the first and third layers are each greater than zero, and wherein the ratio of the first average thickness of the second layer to the second average thickness of the second layer is at least 2:1, 4:1, 6:1, 8:1, 10:1, 20:1, 30:1, 40:1, 50:1, 100:1, 150:1, 200:1, or even infinity:1; in some embodiments, in a range from 2:1 to infinity:1, 2:1 to 10:1, 2:1 to 50:1, 2:1 to
- the present disclosure describes a method of making a polymeric multilayer film, the method comprising:
- the method further comprises separating at least two of the three polymeric layers of the polymeric multilayer film having the array of openings from each other. In some embodiments, the method further comprises separating each of the three polymeric layers of the polymeric multilayer film having the array of openings from each other.
- Embodiments of polymeric multilayer film described herein are useful, for example, for acoustic absorption.
- FIGS. 1, 1A, 1B, and 1C are schematics of an exemplary polymeric multilayer films described herein;
- FIGS. 2 and 2A are schematics of an exemplary method for making exemplary polymeric multilayer film described herein;
- FIG. 2B is a schematic of an exemplary polymeric multilayer film described herein.
- exemplary polymeric multilayer film described herein 100 has first and second generally opposed major surfaces 102 , 104 , and first, second, and third layers, 111 , 112 , 113 , an array of blind openings 114 between the first and second major surfaces 102 , 104 , and a thickness, t.
- the first, second, and third layers each have a first average thickness, t 1 , t 2 , and t 3 , respectively (excluding any thickness said first, second, and third layers 111 , 112 , and 113 have in any of the blind openings 114 ).
- the first, second, and third layers each have a second average thickness t 1 ′, t 2 ′, and t 3 ′, respectively, in the blind holes.
- the ratio of the first average thickness of the second layer to the second average thickness of the second layer is at least 2:1.
- the first average thickness of the first layer is at least 25 micrometers; in some embodiments, in a range from 50 micrometers to 200 micrometers.
- the first average thickness of the second layer excluding any thickness the second layer has in any of the blind openings, is at least 25 micrometers; in some embodiments, in a range from 50 micrometers to 500 micrometers.
- the first average thickness of the third layer excluding any thickness the third layers has in any of the blind openings, is at least 25 micrometer; in some embodiments, in a range from 50 micrometers to 200 micrometers, where in t average thicknesses of a layer is determined by an average of 10 measurements.
- the second average thickness of the first layer in the blind holes is not greater than 15 micrometers; in some embodiments, in a range from 0 micrometer to 15 micrometers.
- the second average thickness of the first layer in the blind holes is not greater than 50 micrometers; in some embodiments, in a range from 10 micrometers to 50 micrometers; an in some embodiments the thickness of the second layer in the blind openings is zero.
- the second average thickness of the third layer in the blind holes is not greater than 100 micrometers; in some embodiments, in a range from 10 micrometers to 100 micrometers.
- the ratio of the first average thickness of the second layer to the second average thickness of the second layer is at least 2:1, 4:1, 6:1, 8:1, 10:1, 20:1, 30:1, 40:1, 50:1, 100:1, 150:1, 200:1, or even infinity:1; in some embodiments, in a range from 2:1 to infinity:1, 2:1 to 10:1, 2:1 to 50:1, 2:1 to 100:1, 2:1 to 200:1, 2:1 to infinity:1, 10:1 to 50:1, 10:1 to 100:1, 10:1 to 150:1, 10:1 to 200:1, 10:1 to infinity:1).
- the average thickness of the polymeric multilayer film is greater than 75 micrometers (in some embodiments, greater than 150 micrometers, 200 micrometers, 250 micrometers, 500 micrometers, 750 micrometers, 1000 micrometers, 1500 micrometers, 2000 micrometers, or even at least 2500 micrometers; in some embodiments, in a range from 125 micrometers to 1500 micrometers, or even 125 micrometers to 2500 micrometers).
- the blind openings may be in any of a variety of shapes, including circles and ovals.
- the blind openings have a depth in a range from 15 micrometers to 650 micrometers (in some embodiments, from 50 micrometers to 400 micrometers, 75 micrometers to 300 micrometers, or 100 micrometers to 250 micrometers).
- FIG. 1B shows the exemplary polymeric multilayer film described herein 100 from FIG. 1 after the blind openings ( 114 ) have been opened by a heat source.
- Exemplary polymeric multilayer film 100 a comprises first, second, and third layers 111 a , 112 a , 113 a , and an array of openings 114 a.
- FIG. 1C shows the exemplary polymeric multilayer film 100 a with each of the layers 111 a , 112 a , 113 a from FIG. 1B separated.
- Layer 3113 a has openings 3114 a .
- Layer 3113 b has openings 3114 b .
- Layer 3113 c has openings 3114 c.
- Exemplary polymeric materials for making the polymeric multilayer films include polypropylene and polyurethane.
- at least one of the layers comprises polypropylene and at least another of the layers comprises polyurethane.
- Exemplary polymeric materials for making the polymeric multilayer films include polyamide 6, polyamide 66, polyethyleneterephthalate (PET), copolyester (PETg), cellulose acetobutyrate (CAB), polymethylmethacrylate (PMMA), acrylonitrile butadiene styrene (ABS), polyolefin copolymers, polyethylene, and polystyrene (PS), ethylene vinyl alcohol (EVOH), polycarbonate (PC), polybutyleneterephthalate (PBT), polyethylenenaphthalate (PEN), polypropylene (PP), polyethelyene (PE), polyurethane (TPU), propylene-based interpolymers and ethylene-based interpolymers.
- PET polyethyleneterephthalate
- PETg copolyester
- CAB cellulose acetobutyrate
- PMMA polymethylmethacrylate
- ABS acrylonitrile butadiene styrene
- PS polyolefin copolymers
- suitable material combinations include: linear low density polyethylene (LLDPE) and polyurethane (TPU); medium density polyethylene (MDPE) and polyurethane (TPU); high density polyethylene (HDPE) and polyurethane (TPU); polypropylene and polyurethane (TPU); polystyrene (PS) and polyurethane (TPU); polyethyleneterephthalate (PET) and propylene-based interpolymers; polyethyleneterephthalate (PET) and ethylene-based interpolymers; copolyester (PETg) and propylene-based interpolymers; copolyester (PETg) and ethylene-based interpolymers; acrylonitrile butadiene styrene (ABS) and propylene-based interpolymers; acrylonitrile butadiene styrene (ABS) and ethylene-based interpolymers; polycarbonate (PC) and propylene-based interpolymers; polycarbonate (PC) and
- Suitable polypropylene materials include homo polypropylene and modified polypropylene such as block copolymers, impact copolymer, and random copolymers.
- the first layer comprises at least one of polycarbonate, polyethyleneterephthalate (PET), copolyesters (PETg), polymethylmethacrylate (PMMA) oracrylonitrile butadiene styrene (ABS and the second layer comprises propylene-based interpolymers.
- the first layer comprises polyethylene and the second layer comprises polyurethane (TPU).
- the first layer comprises at least one polyolefin (e.g., polypropylene or polyethylene); wherein the second layer comprises at least one of a polyurethane (including polyurethanes), a propylene interpolymer (including propylene interpolymers), or ethylene interpolymer (including ethylene interpolymers); and wherein the third layer comprises at least one polyolefin (e.g., polypropylene or polyethylene).
- ethylene interpolymers are available, for example, under the trade designation “EXACT” from ExxonMobil, Irving, Tex.; and “ENGAGE” from Dow Chemical Company, Midland, Mich.
- Exemplary propylene interpolymers are available, for example, under the trade designation “VISTAMAXX” from ExxonMobil and “VERSIFY” from Dow Chemical Company.
- FIGS. 2 and 2A are schematics of exemplary methods.
- Three polymeric layers 211 , 212 , 213 are extruded into nip 220 to provide polymeric multilayer film 210 .
- Nip 220 has first roll 221 having structured surface 222 that imparts indentations 214 through first major planar surface 202 of polymeric multilayer film 210 providing blind openings 214 .
- the first major planar surface 202 of polymeric multilayer film 210 having indentations is processed over chill roll 225 while applying heat source 226 to generally opposed second major surface 204 of polymeric multilayer film 210 .
- the application of heat from heat source 226 e.g., a flame results in formation of openings 216 in polymeric multilayer film 210 .
- any of the polymeric materials comprising an article described herein may comprise additives such as inorganic fillers, pigments, slip agents, and flame retardants.
- Suitable extrusion apparatuses for making multilayer films described herein should be apparent to those skilled in the art after reviewing the instant disclosure, including the working examples.
- the rolls e.g., 221 , 224 , 225
- the surface of rolls contacting the polymeric material(s) are chrome plated, copper plated, or aluminum.
- Rolls can be chilled, for example using conventional techniques such as water cooling.
- Nip force can be provided, for example, by pneumatic cylinders.
- Exemplary extrusion speeds include those in a range from 3-15 m/min. (in some embodiments, in a range from 15-50 m/min, 50-100 m/min., or more).
- Exemplary extrusion temperatures are in range from 200° C.-230° C. (in some embodiments, in a range from 230° C.-260° C., 260-300° C., or greater).
- Embodiments of polymeric multilayer film described herein are useful, for example, for acoustic absorption.
- a polymeric multilayer film having first and second generally opposed major surfaces, and comprising first, second, and third layers, an array of blind openings between the first and second major surfaces, and an average thickness, wherein the first, second, and third layers each have a first average thickness excluding any thickness said first, second, and third layers having in any of the blind openings, wherein the first and second layers extend into the first average thickness of the third layer, wherein each of the first, second, and third layers each have a second average thickness (including a thickness of zero) in the blind holes, wherein the second average thickness of the first and third layers are each greater than zero, and wherein the ratio of the first average thickness of the second layer to the second average thickness of the second layer is at least 2:1, 4:1, 6:1, 8:1, 10:1, 20:1, 30:1, 40:1, 50:1, 100:1, 150:1, 200:1, or even infinity:1; in some embodiments, in a range from 2:1 to infinity:1, 2:1 to 10:1, 2:1 to 50:1, 2:1 to 100:1, 2:1 to 200:1,
- a method of making a polymeric multilayer film of any preceding Embodiment comprising:
- the first layer comprises at least one polyolefin (e.g., polypropylene or polyethylene); wherein the second layer comprises at least one of a polyurethane (including polyurethanes), a propylene interpolymer (including propylene interpolymers), or ethylene interpolymer (including ethylene interpolymers); and wherein the third layer comprises at least one polyolefin (e.g., polypropylene or polyethylene).
- the second layer comprises at least one of a polyurethane (including polyurethanes), a propylene interpolymer (including propylene interpolymers), or ethylene interpolymer (including ethylene interpolymers)
- the third layer comprises at least one polyolefin (e.g., polypropylene or polyethylene).
- a perforated multilayer polymeric film as shown in FIG. 2B was prepared using the following procedures.
- a three layer polymeric film consisting of layers A, B and C was prepared using three extruders to feed a 25 cm wide 3 layer multi-manifold die (obtained under the trade designation “CLOEREN” from Cloeren, Inc., Orange Tex.).
- CLOEREN trade designation from Cloeren, Inc., Orange Tex.
- the extrusion process was done vertically downward into a nip consisting of a tooling roll ( 221 ) and a smooth steel backup roll ( 225 ).
- the extrusion process was configured such that layer A contacted the tooling roll ( 221 ) and layer C contacted the backup roll ( 224 ) as shown schematically in FIG. 2 .
- the polymer for layer A was provided with a 3.2 cm single screw extruder.
- the polymer for layer B was provided with a 3.2 cm single screw extruder.
- the polymer for layer C was provided with a 3.2 cm single screw extruder. Heating zone temperatures for the three extruders is shown in Table 1, below.
- the rpms of the extruders are listed in Table 2, below.
- Layers A ( 211 ) was extruded using a polypropylene impact copolymer resin (obtained under the trade designation “DOW C700-35N 35 MFI” from Dow Chemical Company, Midland, Mich.).
- Layers B ( 212 ) was extruded using a polyurethane resin (obtained under the trade designation “IROGRAN A 78 P 4766” from Huntsman International LLC, Woodlands, Tex.).
- Layer C ( 213 ) was extruded using polypropylene impact copolymer resin (“DOW C700-35N 35 MFI”).
- the basis weight of layer A ( 211 ) was 174 g/m 2 .
- the basis weight of layer B ( 212 ) was 96 g/m 2 .
- the basis weight of layer C ( 213 ) was 92 g/m 2 .
- the two rolls comprising the nip were water cooled rolls ( 221 , 224 ) with a nominal 30.5 cm in diameter and 40.6 cm face widths. Nip force was provided by pneumatic cylinders.
- the smooth steel backup roll ( 224 ) temperature set point of 49° C.
- the tooling roll ( 221 ) had male post features ( 222 ) cut into the surface of the roll.
- the male post features were chrome plated.
- the male features (defined as posts) ( 222 ) on the tool surface were flat square topped pyramids with a square base. The top of the posts were 94 micrometers square and the bases were 500 micrometers square.
- the overall post height was 914 micrometers.
- the center to center spacing of the posts was 820 micrometers in both the radial and cross roll directions.
- the tooling roll ( 221 ) had a temperature set point of 49° C.
- the tooling roll ( 221 ) and backup rolls ( 224 ) were directly driven.
- the nip force between the two nip rolls was 356 Newton per linear centimeter.
- the extrudate takeaway line speed was 2.4 m/min.
- the polymers for the three layers were extruded from the die ( 230 ) directly into the nip ( 220 ) between the tooling ( 221 ) and backup roll ( 224 ).
- the male features ( 222 ) on the tooling roll ( 221 ) created indentations ( 214 ) in the extrudate.
- a thin layer of polymer ( 223 ) remained between the tooling ( 221 ) and backup roll ( 224 ). Typically this layer ( 223 ) was less than 20 micrometer thick.
- the extrudate remained on the tooling roll ( 221 ) for 180 degrees of wrap to chill and solidify the extrudate into a multilayer polymeric film.
- Layers A ( 211 ), B ( 212 ), and C ( 213 ) were then separated from each other.
- Layer B ( 212 ) is a perforated film having an array of holes.
- a perforated multilayer polymeric film as shown in FIG. 2B was prepared using the following procedures.
- a three layer polymeric film consisting of layers A, B and C was prepared using three extruders to feed a 25 cm wide 3 layer multi-manifold die (“CLOEREN”).
- CLOEREN layer multi-manifold die
- the extrusion process was done vertically downward into a nip consisting of a tooling roll ( 221 ) and a smooth steel backup roll ( 224 ).
- the extrusion process was configured such that layer A contacted the tooling roll ( 221 ) and layer C contacted the backup roll ( 224 ) as shown schematically in FIG. 2 .
- the polymer for layer A was provided with a 3.2 cm single screw extruder.
- the polymer for layer B was provided with a 3.2 cm single screw extruder.
- the polymer for layer C was provided with a 3.2 cm single screw extruder. Heating zone temperatures for the three extruders is shown in Table 3, below.
- Layers A and C ( 211 , 213 ) was extruded using a polycarbonate resin (obtained under the trade designation “BAYER MAKROLON 2447” from Bayer Material Science, Pittsburgh, Pa.).
- Layers B ( 212 ) was extruded using an ethylene-based interpolymer resin (obtained under the trade designation “ENGAGE 8411” from Dow Chemical Company).
- the basis weight of layer A ( 211 ) was 232 g/m 2 .
- the basis weight of layer B ( 212 ) was 56 g/m 2 .
- the basis weight of layer C ( 213 ) was 130 g/m 2 .
- the two rolls comprising the nip were water cooled rolls ( 221 , 224 ) with a nominal 30.5 cm in diameter and 40.6 cm face widths. Nip force was provided by pneumatic cylinders.
- the smooth steel backup roll ( 224 ) temperature set point of 38° C.
- the tooling roll ( 221 ) had male post features ( 222 ) cut into the surface of the roll.
- the male post features were chrome plated.
- the male features (defined as posts) ( 222 ) on the tool surface were flat square topped pyramids with a square base. The top of the posts were 94 micrometers square and the bases were 500 micrometers square.
- the overall post height was 914 micrometers.
- the center to center spacing of the posts was 820 micrometers in both the radial and cross roll directions.
- the tooling roll ( 221 ) had a temperature set point of 38° C.
- the tooling roll ( 221 ) and backup roll ( 224 ) were directly driven.
- the nip force between the two nip rolls was 356 Newton per linear centimeter.
- the extrudate takeaway line speed was 3.0 m/min.
- the polymers for the three layers were extruded from the die ( 230 ) directly into the nip ( 220 ) between the tooling ( 221 ) and backup roll ( 224 ).
- the male features ( 222 ) on the tooling roll ( 221 ) created indentations ( 214 ) in the extrudate.
- a thin layer of polymer ( 223 ) remained between the tooling ( 221 ) and backup roll ( 224 ). Typically this layer ( 223 ) was less than 20 micrometer thick.
- the extrudate remained on the tooling roll ( 221 ) for 180 degrees of wrap to chill and solidify the extrudate into a multilayer polymeric film.
- Layers A ( 211 ), B ( 212 ) and C ( 213 ) were then separated from each other.
- Layer B ( 212 ) is a perforated film having an array of holes.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Laminated Bodies (AREA)
- Shaping Of Tube Ends By Bending Or Straightening (AREA)
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US15/038,880 US20170001359A1 (en) | 2013-12-12 | 2014-12-09 | Polymeric multilayer films and methods to make the same |
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US20160023393A1 (en) * | 2013-03-12 | 2016-01-28 | 3M Innovative Properties Company | Method of making polymeric multilayer films |
US20170013581A1 (en) * | 2014-03-21 | 2017-01-12 | Huawei Technologies Co., Ltd. | Method and apparatus for configuring position of frequency resource |
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WO2015088773A1 (en) | 2013-12-12 | 2015-06-18 | 3M Innovative Properties Company | Method of making polymeric multilayer films |
EP3548275A1 (en) * | 2016-11-30 | 2019-10-09 | 3M Innovative Properties Company | Polymeric multilayer film with openings |
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- 2014-12-09 CN CN201480067597.XA patent/CN105813834B/zh active Active
- 2014-12-09 EP EP14830906.5A patent/EP3079897B1/en active Active
- 2014-12-09 KR KR1020167018252A patent/KR102322969B1/ko active IP Right Grant
- 2014-12-09 WO PCT/US2014/069266 patent/WO2015089024A1/en active Application Filing
- 2014-12-09 US US15/038,880 patent/US20170001359A1/en not_active Abandoned
- 2014-12-09 JP JP2016538763A patent/JP6807230B2/ja active Active
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EP3079897A1 (en) | 2016-10-19 |
WO2015089024A1 (en) | 2015-06-18 |
KR102322969B1 (ko) | 2021-11-08 |
CN105813834A (zh) | 2016-07-27 |
KR20160098316A (ko) | 2016-08-18 |
EP3079897B1 (en) | 2020-11-18 |
CN105813834B (zh) | 2018-10-16 |
JP6807230B2 (ja) | 2021-01-06 |
JP2017503682A (ja) | 2017-02-02 |
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